EP3124455A1 - Method for the production of a fibre-reinforced carbon-ceramic composite material, composite carbon-ceramic material obtained using such method and component of a disc brake made of such material - Google Patents
Method for the production of a fibre-reinforced carbon-ceramic composite material, composite carbon-ceramic material obtained using such method and component of a disc brake made of such material Download PDFInfo
- Publication number
- EP3124455A1 EP3124455A1 EP16182028.7A EP16182028A EP3124455A1 EP 3124455 A1 EP3124455 A1 EP 3124455A1 EP 16182028 A EP16182028 A EP 16182028A EP 3124455 A1 EP3124455 A1 EP 3124455A1
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- European Patent Office
- Prior art keywords
- mixture
- cellulose
- weight
- semi
- finished product
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
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- 238000000034 method Methods 0.000 title claims abstract description 55
- 239000002131 composite material Substances 0.000 title claims abstract description 35
- 229910010293 ceramic material Inorganic materials 0.000 title claims abstract description 33
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 31
- 239000000463 material Substances 0.000 title claims abstract description 17
- 239000000919 ceramic Substances 0.000 title description 3
- 239000000203 mixture Substances 0.000 claims abstract description 97
- 239000011265 semifinished product Substances 0.000 claims abstract description 41
- 239000011230 binding agent Substances 0.000 claims abstract description 38
- 239000001913 cellulose Substances 0.000 claims abstract description 37
- 229920002678 cellulose Polymers 0.000 claims abstract description 37
- 229920000609 methyl cellulose Polymers 0.000 claims abstract description 37
- 239000001923 methylcellulose Substances 0.000 claims abstract description 37
- 235000010981 methylcellulose Nutrition 0.000 claims abstract description 37
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 30
- 239000010703 silicon Substances 0.000 claims abstract description 30
- 230000008595 infiltration Effects 0.000 claims abstract description 19
- 238000001764 infiltration Methods 0.000 claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 230000003014 reinforcing effect Effects 0.000 claims abstract description 15
- 238000010304 firing Methods 0.000 claims abstract description 8
- 230000004927 fusion Effects 0.000 claims abstract description 4
- 229920005989 resin Polymers 0.000 claims description 23
- 239000011347 resin Substances 0.000 claims description 23
- 238000000197 pyrolysis Methods 0.000 claims description 20
- 239000000843 powder Substances 0.000 claims description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 12
- 229920001568 phenolic resin Polymers 0.000 claims description 11
- 239000005011 phenolic resin Substances 0.000 claims description 11
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 claims description 10
- 239000000945 filler Substances 0.000 claims description 10
- 239000000654 additive Substances 0.000 claims description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 6
- 230000000996 additive effect Effects 0.000 claims description 6
- 239000000571 coke Substances 0.000 claims description 5
- 229910010271 silicon carbide Inorganic materials 0.000 claims description 5
- 229910002804 graphite Inorganic materials 0.000 claims description 4
- 239000010439 graphite Substances 0.000 claims description 4
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims description 4
- 239000005995 Aluminium silicate Substances 0.000 claims description 3
- 229910052582 BN Inorganic materials 0.000 claims description 3
- PZNSFCLAULLKQX-UHFFFAOYSA-N Boron nitride Chemical compound N#B PZNSFCLAULLKQX-UHFFFAOYSA-N 0.000 claims description 3
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims description 3
- 229910052581 Si3N4 Inorganic materials 0.000 claims description 3
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 3
- 239000004411 aluminium Substances 0.000 claims description 3
- 229910052782 aluminium Inorganic materials 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- 235000012211 aluminium silicate Nutrition 0.000 claims description 3
- 239000011651 chromium Substances 0.000 claims description 3
- 229910052804 chromium Inorganic materials 0.000 claims description 3
- 239000004927 clay Substances 0.000 claims description 3
- 229910052742 iron Inorganic materials 0.000 claims description 3
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims description 3
- 229910052751 metal Inorganic materials 0.000 claims description 3
- 239000002184 metal Substances 0.000 claims description 3
- 150000002739 metals Chemical class 0.000 claims description 3
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 claims description 3
- 238000007669 thermal treatment Methods 0.000 claims description 3
- 239000010936 titanium Substances 0.000 claims description 3
- 229910052719 titanium Inorganic materials 0.000 claims description 3
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 22
- 229910052799 carbon Inorganic materials 0.000 description 9
- 239000003822 epoxy resin Substances 0.000 description 5
- 229920000647 polyepoxide Polymers 0.000 description 5
- 238000007796 conventional method Methods 0.000 description 4
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- 239000003795 chemical substances by application Substances 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 230000004931 aggregating effect Effects 0.000 description 2
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- 238000006243 chemical reaction Methods 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
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- 238000005265 energy consumption Methods 0.000 description 2
- 239000003999 initiator Substances 0.000 description 2
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- 229920002239 polyacrylonitrile Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
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- 206010017076 Fracture Diseases 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
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- 239000002245 particle Substances 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 229920000768 polyamine Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
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- 238000002360 preparation method Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000011208 reinforced composite material Substances 0.000 description 1
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- C04B35/515—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics
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- C04B35/573—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbides or oxycarbides based on silicon carbide obtained by reaction sintering or recrystallisation
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- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
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- F16D65/126—Discs; Drums for disc brakes characterised by the material used for the disc body the material being of low mechanical strength, e.g. carbon, beryllium; Torque transmitting members therefor
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- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/02—Composition of constituents of the starting material or of secondary phases of the final product
- C04B2235/50—Constituents or additives of the starting mixture chosen for their shape or used because of their shape or their physical appearance
- C04B2235/54—Particle size related information
- C04B2235/5463—Particle size distributions
- C04B2235/5472—Bimodal, multi-modal or multi-fraction
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/60—Aspects relating to the preparation, properties or mechanical treatment of green bodies or pre-forms
- C04B2235/604—Pressing at temperatures other than sintering temperatures
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/60—Aspects relating to the preparation, properties or mechanical treatment of green bodies or pre-forms
- C04B2235/608—Green bodies or pre-forms with well-defined density
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/60—Aspects relating to the preparation, properties or mechanical treatment of green bodies or pre-forms
- C04B2235/616—Liquid infiltration of green bodies or pre-forms
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16D—COUPLINGS FOR TRANSMITTING ROTATION; CLUTCHES; BRAKES
- F16D2200/00—Materials; Production methods therefor
- F16D2200/0034—Materials; Production methods therefor non-metallic
- F16D2200/0039—Ceramics
- F16D2200/0047—Ceramic composite, e.g. C/C composite infiltrated with Si or B, or ceramic matrix infiltrated with metal
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16D—COUPLINGS FOR TRANSMITTING ROTATION; CLUTCHES; BRAKES
- F16D2200/00—Materials; Production methods therefor
- F16D2200/006—Materials; Production methods therefor containing fibres or particles
- F16D2200/0065—Inorganic, e.g. non-asbestos mineral fibres
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16D—COUPLINGS FOR TRANSMITTING ROTATION; CLUTCHES; BRAKES
- F16D2200/00—Materials; Production methods therefor
- F16D2200/006—Materials; Production methods therefor containing fibres or particles
- F16D2200/0073—Materials; Production methods therefor containing fibres or particles having lubricating properties
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16D—COUPLINGS FOR TRANSMITTING ROTATION; CLUTCHES; BRAKES
- F16D2200/00—Materials; Production methods therefor
- F16D2200/0082—Production methods therefor
Definitions
- the present invention relates to a method for the production of a composite, fibre-reinforced carbon-ceramic material, and composite carbon-ceramic material obtained using such method.
- the present invention relates to a method for the production of a composite, fibre-reinforced carbon-ceramic material, and composite carbon-ceramic material obtained using such method.
- This material has properties of chemical and thermal resistance, as well as a lightness which makes it particularly suitable for use in the industrial field, and in particular in the automotive and aeronautical industries, as a substitute for metal materials.
- the present invention thus also relates to a component of a disc brake made of such material, and in particular a brake disc.
- CCM carbon-ceramic composite materials
- CCM carbon-ceramic composite materials
- these composite carbon-ceramic materials are produced by mixing reinforcing fibres with an aggregating resin and other additives and placing the mixture thus obtained in a mould, where it is formed by heating and the application of pressure to obtain a shaped semi-finished product.
- the semi-finished product is then subjected to a first firing in a furnace at a temperature such as to bring about the carbonisation or pyrolysis of the resin.
- a temperature such as to bring about the carbonisation or pyrolysis of the resin.
- the semi-finished product acquires a certain porosity because of the loss of volatile material at the carbonisation or pyrolysis temperatures.
- the fired semi-finished product is subjected to a second firing in the presence of silicon at a temperature such as to cause the melting of the silicon and its infiltration in the pores of the aforesaid semi-finished product.
- the infiltration of the silicon increases the cohesion of the carbon fibres, while at the same time the molten silicon, in the conditions of the second firing, reacts in part with the carbon of the semi-finished product, forming silicon carbides which have the effect of improving the cohesion characteristics of the material.
- the composite material prepared using the process described above is often used in the production of brake and clutch components for vehicles, in particular for disc brakes, thanks to its characteristics of good resistance to compression, at the temperature generated by friction and wear.
- composition of epoxy resin or a phenolic resin comprising the following components is used as aggregating resin: epoxy or phenolic resin; a radical polymerisable monomer; a radical polymerisation initiator; and an amine-based hardening agent.
- compositions of epoxy or phenolic resins are characterised by high viscosity and low fluidity at ambient temperature. This makes the hot forming of the mixture necessary as well as the subsequent heating step of the shaped semi-finished product (green body) to allow the polymerisation of the resin, this step being essential to give form and consistency to the semi-finished product. All these steps, together with the subsequent pyrolysis and carbonisation treatment, contribute to making the production process of carbon-ceramic materials extremely expensive due to the high energy absorption and the long processing cycles required for the polymerisation and pyrolysis of the material.
- the purpose of the present invention is to eliminate, or at least reduce, the aforementioned problems relative to the prior art, by providing a production method of a composite, fibre-reinforced carbon-ceramic material which permits increased productivity in terms of energy saving and production times, obtaining a final composite carbon-ceramic material having comparable properties to the materials made using conventional methods.
- the method for the production of a composite, fibre-reinforced carbon-ceramic material comprises at least the following operating steps:
- the aforesaid organic agglomerating binder essential for the forming of such material, is present between 15% and 25% by weight of said mixture and comprises cellulose, methyl cellulose or a mixture of cellulose and methyl cellulose and is added to the mixture together with water.
- the forming step is conducted at a temperature not exceeding 100°C.
- said forming step may be conducted for a period of time not exceeding 10 minutes, and preferably between 5 and 10 minutes.
- the forming step is conducted by exerting a pressure of between 20 and 100 kg / cm 2 on the mixture inside the mould.
- the aforesaid organic agglomerating binder is added to the mixture in powder form.
- the water is added to the mixture in a nebulised form.
- the aforesaid organic agglomerating binder additive consists only of cellulose, methyl cellulose or a mixture of cellulose and methyl cellulose.
- the aforesaid mixture comprises:
- the step b) is conducted at a temperature not exceeding 50°C, preferably at ambient temperature.
- the forming step b) can be conducted at a temperature between 50°C and 100°C to give greater consistency to the semi-finished product.
- the step c) of infiltration with molten silicon is conducted immediately after the forming step b), without intermediate thermal treatments.
- the aforesaid organic agglomerating binder additive comprises: cellulose, methylcellulose or a mixture of cellulose and methylcellulose; and an organic binder resin.
- the aforesaid organic binder resin is a phenolic resin.
- the aforesaid mixture comprises:
- the forming step b) is conducted at a temperature between 50 °C and 100 °C.
- the infiltration step c) with molten silicon is preceded by a step d) of pyrolysis of the semi-finished product obtained at the end of the forming step b).
- the aforesaid pyrolysis step d) is conducted for a period of time not exceeding 120 minutes, and preferably between 30 and 60 minutes.
- the said mixture comprises at least 20% by weight of powder fillers, selected from the group consisting of coke, silicon carbide, graphite or a mixture thereof.
- the mixture may comprise up to 5% by weight of a component selected from the group consisting of: boron nitride; silicon nitride; kaolin; clay; or metals, such as titanium, chromium, iron, aluminium; or a mixture thereof.
- a component selected from the group consisting of: boron nitride; silicon nitride; kaolin; clay; or metals, such as titanium, chromium, iron, aluminium; or a mixture thereof.
- the present invention relates to a composite carbon-ceramic material, characterised in that it is made using the production method according to the invention.
- the present invention relates to a component of a disc brake, characterised in that it is made at least in part with a composite carbon-ceramic material made using the production method according to the invention.
- the aforesaid component of a disc brake is a brake disc.
- the method according to the present invention makes it possible to produces a composite fibre-reinforced carbon-ceramic material with properties of chemical and thermal resistance, as well as a lightness which makes it particularly suitable for use in the industrial field, and in particular in the automotive and aeronautical industries, as a substitute for metal materials.
- the method for the production of a composite, fibre-reinforced carbon-ceramic material comprises at least the following operating steps:
- the forming of the mixture may be carried out using a mould or by using a sheet-forming process, in particular with winding of the mixture in the form of a sheet around a mandrel.
- the aforesaid organic agglomerating binder essential for the forming of such material, is present between 15% and 25% by weight of said mixture and comprises cellulose, methyl cellulose or a mixture of cellulose and methyl cellulose and is added to the mixture together with water.
- the present invention is based on having surprisingly found that the use of cellulose, methylcellulose or a mixture of such two compounds as the organic agglomerating binder in place of conventional binding resins (in particular phenolic) or at least in partial substitution of the same makes it possible to:
- the aforesaid forming step is conducted at a temperature not exceeding 100°C.
- the method according to the present invention permits a "substantially cold” forming (or moulding) to be carried out, "substantially cold” meaning a process conducted at temperatures not far from ambient temperature or (in relative terms) significantly lower than the conventionally required temperatures.
- a temperature not less than 150°C to a temperature of not more than 100 °C.
- the forming step can be conducted even at a temperature lower than 50°C, and in particular at ambient temperature.
- "Ambient temperature” means a temperature around 25°C.
- the temperature at which the forming step can be conducted depends on the composition of the organic agglomerating binder, and in particular on the use or not of an organic binder resin. In the case where only cellulose, methylcellulose or a mixture of two such compounds is used as the organic agglomerating binder it is possible to perform the forming step at temperatures below 50°C.
- said forming step may be conducted for a period of time not exceeding 10 minutes, and preferably between 5 and 10 minutes, obtaining a semi-finished product of a good consistency which can be handled directly without loss in terms of shape or size.
- a semi-finished product of a good consistency which can be handled directly without loss in terms of shape or size.
- the method according to the invention thus makes it possible to significantly reduce not only the forming temperature, but also the process times.
- the forming step is conducted by exerting a pressure of between 20 and 100 kg / cm 2 on the mixture inside the mould.
- the aforesaid organic agglomerating binder (in the presence or absence of an organic resin binder) is added to the mixture in powder form. This allows a better distribution of the agglomerating binder in the mixture and a quicker fluidification of the mixture.
- the water is added to the mixture in a nebulised form.
- This makes it possible to speed up the interaction between the agglomerating binder and the water, and in particular between the cellulose, methylcellulose or a mixture of such two compounds and the water, so as to favour the distribution of the agglomerating binder in the mixture and the fluidification of said mixture.
- the water essentially performs the function of favouring the mixture of the powders, and in particular of the cellulose, methylcellulose or mixture thereof with the other components.
- filaments composed substantially of carbon are used as a reinforcing fibre.
- filaments composed substantially of carbon is intended to include, in particular, fibrous materials obtained by pyrolysis of various products of synthetic origin, for example, polyacrylonitrile (PAN) and polisilazane, or of natural origin, for example, tars, cellulose-based natural sources such as vegetable fibres and wood.
- PAN polyacrylonitrile
- polisilazane or of natural origin, for example, tars, cellulose-based natural sources such as vegetable fibres and wood.
- the reinforcing fibres may be previously coated with a protective resin, preferably polyurethane, before being used in the method according to the invention.
- a protective resin preferably polyurethane
- the reinforcing fibres may be previously coated with the same organic agglomerating binder used for the preparation of the mixture. This way a greater cohesion of the material and a more compact product is obtained.
- the aforesaid organic agglomerating binder additive consists only of cellulose, methyl cellulose or a mixture of cellulose and methyl cellulose.
- the mixture does not contain an organic binder resin, and in particular does not contain phenolic resin.
- the aforesaid mixture comprises:
- the mixture comprises at least 20% by weight of powder fillers, selected from the group consisting of coke, silicon carbide, graphite or a mixture thereof.
- the step b) is conducted at a temperature not exceeding 50°C, preferably at ambient temperature.
- the forming step can be conducted at a temperature between 50 °C and 100 °C.
- the infiltration step c) with molten silicon is conducted immediately after the forming step b), without intermediate thermal treatments.
- the production method does not comprise an intermediate stage of pyrolysis and the semi-finished product obtained at the end of the forming step b) is directly subjected to infiltration with silicon.
- the semi-finished product obtained at the end of the forming step b) has a good consistency and density of the order of 1.0-1.1 g/cm 3 .
- the semi-finished product can be easily handled without any particular risk of fractures and can be transferred directly from the mould into the furnace for infiltration.
- the production method has been tested with a mixture having the following composition: 40% fibre, 34% of coke in powder of different particle sizes, 20% of methyl cellulose powder, 10% water, 6% of additives. Carbon fibres are used as fibre.
- the powder components were mixed with each other gradually; to this powder mixture the fibres and the water in nebulised form were added.
- the mixture thus obtained was uniaxially pressed in a mould at a pressure of about 68 kg/cm 2 at a temperature of 25°C for 10 minutes.
- the semi-finished product obtained at the end of the forming step showed good consistency such as to allow its manipulation without loss of form and size and had a density of the order of 1.0-1.1 g/cm 3 .
- the composite carbon-ceramic material obtained at the end of the infiltration step (conducted directly on the semi-finished product obtained from the forming step without intermediate pyrolysis) presented good characteristics of mechanical resistance.
- the aforesaid organic agglomerating binder additive comprises: cellulose, methylcellulose or a mixture of cellulose and methylcellulose; and an organic binder resin.
- the aforesaid organic binder resin is a phenolic resin.
- the aforesaid mixture comprises:
- the mixture comprises at least 20% by weight of powder fillers, selected from the group consisting of coke, silicon carbide, graphite or a mixture thereof.
- the forming step b) is conducted at a temperature between 50°C and 100 °C.
- the infiltration step c) with molten silicon is preceded by a step d) of pyrolysis of the semi-finished product obtained at the end of the forming step b).
- the aforesaid pyrolysis step d) is conducted for a period of time not exceeding 120 minutes, and preferably between 30 and 60 minutes.
- the use in the mixture of the organic binder resin, and in particular of the phenolic resin makes it possible to increase the density of the semi-finished product obtained at the end of the forming step b). It passes from a density of 1.0- 1.1g/cm 3 to density values of 1.4- 1.5 g/cm 3 .
- the use in the mixture of the organic binder resin, and in particular the phenolic resin, also makes it possible to limit the infiltration of silicon in the material, with consequent protection of the carbon fibres from the reaction with the silicon.
- the amount of phenolic resin introduced to the mixture is therefore considerably lower than the amount provided for in the conventional methods. In fact, a quantity not exceeding 10% by weight is provided for against the amount not less than 35-40% by weight traditionally provided for.
- the use of the organic binder resin (in particular) of the phenolic resin does not affect the process times of the forming step b) which remain substantially unchanged (no greater than 10 minutes).
- Use of the resin requires the following however:
- the times of the additional step d) of pyrolysis are, however, very low (in the order of 1-2 hours) and in any case lower than the conventional methods, which provide for pyrolysis steps lasting several hours, typically between 8 and 24 hours.
- the mixture may comprise a component selected from the group consisting of: boron nitride; silicon nitride; kaolin; clay; or metals, such as titanium, chromium, iron, aluminium; or a mixture thereof.
- Such one or more components are added in said mixture in powder form.
- such one or more components are present in the mixture in an amount not exceeding 5% by weight.
- the introduction in the mixture of such components makes it possible to increase the density of the semi-finished product obtained at the end of the forming step b) and to reduce the infiltration of silicon in the semi-finished product, with consequent protection of the carbon fibres from the reaction with the silicon.
- the present invention relates to a composite carbon-ceramic material, characterised in that it is made with the production method according to the invention, and in particular as described above.
- the present invention relates to a component of a disc brake, characterised in that it is made at least in part with a composite carbon-ceramic material made using the production method according to the invention, and in particular as described above.
- the aforesaid component of a disc brake is a brake disc.
- the invention permits several advantages to be achieved, in part already described.
- the production method of a composite, fibre-reinforced carbon-ceramic material according to the present invention permits increased productivity in terms of energy saving and production times, obtaining a final composite carbon-ceramic material having comparable properties to the materials obtained with conventional methods.
- the forming step can be carried out in very short times and at temperatures not exceeding 100 °C.
- the composite carbon-ceramic material without subjecting the semi-finished product obtained in the forming step to pyrolysis.
- the moulded semi-finished product can pass directly to the infiltration step with silicon. This entails a further reduction in costs and production times.
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Abstract
Description
- The present invention relates to a method for the production of a composite, fibre-reinforced carbon-ceramic material, and composite carbon-ceramic material obtained using such method.
- The present invention relates to a method for the production of a composite, fibre-reinforced carbon-ceramic material, and composite carbon-ceramic material obtained using such method.
- This material has properties of chemical and thermal resistance, as well as a lightness which makes it particularly suitable for use in the industrial field, and in particular in the automotive and aeronautical industries, as a substitute for metal materials. The present invention thus also relates to a component of a disc brake made of such material, and in particular a brake disc.
- The use of carbon-ceramic composite materials (CCM) is well-known in many applications where a high resistance to impact, compression and temperature generated by friction is required, characteristics which cannot be guaranteed by simple ceramic materials because of their inherent fragility.
- In particular, carbon-ceramic composite materials (CCM) for applications in braking systems are known of, obtained by the interaction of silicon with a mixture comprising carbon fibres and additives at a temperature in which the silicon is in the molten state.
- Generally, these composite carbon-ceramic materials are produced by mixing reinforcing fibres with an aggregating resin and other additives and placing the mixture thus obtained in a mould, where it is formed by heating and the application of pressure to obtain a shaped semi-finished product. The semi-finished product is then subjected to a first firing in a furnace at a temperature such as to bring about the carbonisation or pyrolysis of the resin. As a result of this firing, the semi-finished product acquires a certain porosity because of the loss of volatile material at the carbonisation or pyrolysis temperatures. Subsequently, the fired semi-finished product is subjected to a second firing in the presence of silicon at a temperature such as to cause the melting of the silicon and its infiltration in the pores of the aforesaid semi-finished product. The infiltration of the silicon increases the cohesion of the carbon fibres, while at the same time the molten silicon, in the conditions of the second firing, reacts in part with the carbon of the semi-finished product, forming silicon carbides which have the effect of improving the cohesion characteristics of the material.
- The composite material prepared using the process described above is often used in the production of brake and clutch components for vehicles, in particular for disc brakes, thanks to its characteristics of good resistance to compression, at the temperature generated by friction and wear.
- Generally, in the production of composite carbon-ceramic materials for the automotive or aeronautical industry a composition of epoxy resin or a phenolic resin comprising the following components is used as aggregating resin: epoxy or phenolic resin; a radical polymerisable monomer; a radical polymerisation initiator; and an amine-based hardening agent.
- Such compositions of epoxy or phenolic resins are characterised by high viscosity and low fluidity at ambient temperature. This makes the hot forming of the mixture necessary as well as the subsequent heating step of the shaped semi-finished product (green body) to allow the polymerisation of the resin, this step being essential to give form and consistency to the semi-finished product. All these steps, together with the subsequent pyrolysis and carbonisation treatment, contribute to making the production process of carbon-ceramic materials extremely expensive due to the high energy absorption and the long processing cycles required for the polymerisation and pyrolysis of the material.
- In the field of composite carbon-ceramic materials a need therefore exists to significantly reduce production costs, by intervening both on processing times and on energy consumption.
- In the Japanese patent application no.
2006-265434 - In the patent application
US 8883938 a method is proposed for producing a fibre-reinforced composite material having good mechanical properties starting from a composition having excellent fluidity already at a temperature of 100 °C. The essential components of such composition are an epoxy resin, a radical polymerisable monomer containing an acid group, a radical polymerisation initiator and an amine-based hardening agent. The production method uses a vacuum resin transfer moulding (RTM) process, with different pressures in the cavity and outside. Nevertheless, the method has a high energy consumption related to the pre-heating of the green body and the subsequent pyrolysis. Moreover, this method does not allow control of the orientation of the reinforcing fibres or much freedom in the structuring of the final material. - Consequently, the purpose of the present invention is to eliminate, or at least reduce, the aforementioned problems relative to the prior art, by providing a production method of a composite, fibre-reinforced carbon-ceramic material which permits increased productivity in terms of energy saving and production times, obtaining a final composite carbon-ceramic material having comparable properties to the materials made using conventional methods.
- Such drawbacks are resolved by a production method of a composite, fibre-reinforced carbon-ceramic material according to claim 1.
- According to a general form of implementation of the invention, the method for the production of a composite, fibre-reinforced carbon-ceramic material (CCM) comprises at least the following operating steps:
- a) preparing a mixture comprising at least reinforcing fibres and an organic agglomerating binder;
- b) forming the mixture to obtain a semi-finished product;
- c) infiltrating the semi-finished product with molten silicon, subjecting the semi-finished product to a firing in the presence of silicon at a temperature such as substantially to bring about the fusion of said silicon and its infiltration into said semi-finished product thus obtaining a composite, fibre-reinforced carbon-ceramic material (CCM).
- The aforesaid organic agglomerating binder, essential for the forming of such material, is present between 15% and 25% by weight of said mixture and comprises cellulose, methyl cellulose or a mixture of cellulose and methyl cellulose and is added to the mixture together with water.
- The forming step is conducted at a temperature not exceeding 100°C.
- Preferably, said forming step may be conducted for a period of time not exceeding 10 minutes, and preferably between 5 and 10 minutes.
- Advantageously, the forming step is conducted by exerting a pressure of between 20 and 100 kg / cm2 on the mixture inside the mould.
- Preferably, the aforesaid organic agglomerating binder is added to the mixture in powder form.
- Advantageously, the water is added to the mixture in a nebulised form.
- According to a preferred form of implementation of the invention, the aforesaid organic agglomerating binder additive consists only of cellulose, methyl cellulose or a mixture of cellulose and methyl cellulose.
- In particular, according to said preferred form of implementation of the method, the aforesaid mixture comprises:
- between 35% and 50% by weight of reinforcing fibres;
- between 15% and 25% by weight of cellulose, methylcellulose or a mixture of cellulose and methylcellulose;
- at least 20% by weight of fillers; and
- up to 10% by weight of water.
- Advantageously, according to said preferred form of implementation of the method, the step b) is conducted at a temperature not exceeding 50°C, preferably at ambient temperature.
- Alternatively, the forming step b)can be conducted at a temperature between 50°C and 100°C to give greater consistency to the semi-finished product.
- Advantageously, again according to said preferred form of implementation of the method, the step c) of infiltration with molten silicon is conducted immediately after the forming step b), without intermediate thermal treatments.
- According to an alternative form of implementation of the invention, the aforesaid organic agglomerating binder additive comprises: cellulose, methylcellulose or a mixture of cellulose and methylcellulose; and an organic binder resin.
- Preferably, the aforesaid organic binder resin is a phenolic resin.
- In particular, according to said alternative form of implementation of the method, the aforesaid mixture comprises:
- between 35% and 50% by weight of reinforcing fibres;
- between 5% and 15% by weight of cellulose, methylcellulose or a mixture of cellulose and methylcellulose;
- not more than 10% by weight of organic resin binder;
- at least 20% of fillers; and
- up to 10% by weight of water.
- Advantageously, again according to said alternative form of implementation of the method, the forming step b) is conducted at a temperature between 50 °C and 100 °C.
- Preferably, again according to said alternative form of implementation of the method, the infiltration step c) with molten silicon is preceded by a step d) of pyrolysis of the semi-finished product obtained at the end of the forming step b).
- Advantageously, the aforesaid pyrolysis step d) is conducted for a period of time not exceeding 120 minutes, and preferably between 30 and 60 minutes.
- Preferably, both with reference to the preferred and the alternative forms of implementation, the said mixture comprises at least 20% by weight of powder fillers, selected from the group consisting of coke, silicon carbide, graphite or a mixture thereof.
- Advantageously, the mixture may comprise up to 5% by weight of a component selected from the group consisting of: boron nitride; silicon nitride; kaolin; clay; or metals, such as titanium, chromium, iron, aluminium; or a mixture thereof. One or more of these components are added to the mixture in powder form.
- The present invention relates to a composite carbon-ceramic material, characterised in that it is made using the production method according to the invention.
- The present invention relates to a component of a disc brake, characterised in that it is made at least in part with a composite carbon-ceramic material made using the production method according to the invention.
- Preferably, the aforesaid component of a disc brake is a brake disc.
- The technical characteristics of the invention can be seen clearly from the contents of the following claims and the advantages of the same will be more clearly comprehensible from the detailed description below,
- The method according to the present invention makes it possible to produces a composite fibre-reinforced carbon-ceramic material with properties of chemical and thermal resistance, as well as a lightness which makes it particularly suitable for use in the industrial field, and in particular in the automotive and aeronautical industries, as a substitute for metal materials.
- According to a general form of implementation of the invention, the method for the production of a composite, fibre-reinforced carbon-ceramic material comprises at least the following operating steps:
- a) preparing a mixture comprising at least reinforcing fibres and an organic agglomerating binder;
- b) forming the mixture to obtain a semi-finished product;
- c) infiltrating the semi-finished product with molten silicon, subjecting the semi-finished product to a firing in the presence of silicon at a temperature such as substantially to bring about the fusion of said silicon and its infiltration into said semi-finished product thus obtaining a composite, fibre-reinforced carbon-ceramic material,
- The forming of the mixture may be carried out using a mould or by using a sheet-forming process, in particular with winding of the mixture in the form of a sheet around a mandrel.
- The aforesaid organic agglomerating binder, essential for the forming of such material, is present between 15% and 25% by weight of said mixture and comprises cellulose, methyl cellulose or a mixture of cellulose and methyl cellulose and is added to the mixture together with water.
- As described further below, the present invention is based on having surprisingly found that the use of cellulose, methylcellulose or a mixture of such two compounds as the organic agglomerating binder in place of conventional binding resins (in particular phenolic) or at least in partial substitution of the same makes it possible to:
- significantly lower the temperature at which the forming step of the mixture can be performed;
- significantly reduce the length of the forming step;
- eliminate the step of pyrolysis, or at least significantly reduce the execution time thereof.
- All this leads to a reduction of production costs, in terms of process time, energy costs and simplification of the process and of the production plants.
- According to the aforesaid general form of implementation of the invention, the aforesaid forming step is conducted at a temperature not exceeding 100°C.
- In other words, taking into account the significant reduction of the temperature of the forming step compared to conventional production methods of composite, fibre-reinforced, carbon-ceramic materials (CCM), it can be stated -qualitatively- that the method according to the present invention permits a "substantially cold" forming (or moulding) to be carried out, "substantially cold" meaning a process conducted at temperatures not far from ambient temperature or (in relative terms) significantly lower than the conventionally required temperatures. For the forming step in fact, one passes from a temperature not less than 150°C to a temperature of not more than 100 °C.
- Advantageously, as described further below, the forming step can be conducted even at a temperature lower than 50°C, and in particular at ambient temperature. "Ambient temperature" means a temperature around 25°C.
- As described further below, the temperature at which the forming step can be conducted depends on the composition of the organic agglomerating binder, and in particular on the use or not of an organic binder resin. In the case where only cellulose, methylcellulose or a mixture of two such compounds is used as the organic agglomerating binder it is possible to perform the forming step at temperatures below 50°C.
- Preferably, said forming step may be conducted for a period of time not exceeding 10 minutes, and preferably between 5 and 10 minutes, obtaining a semi-finished product of a good consistency which can be handled directly without loss in terms of shape or size. For the forming step in fact, one passes from process times of not less than 45 minutes to process times of not more than 10 minutes.
- The method according to the invention thus makes it possible to significantly reduce not only the forming temperature, but also the process times.
- Advantageously, the forming step is conducted by exerting a pressure of between 20 and 100 kg / cm2 on the mixture inside the mould.
- Preferably, the aforesaid organic agglomerating binder (in the presence or absence of an organic resin binder) is added to the mixture in powder form. This allows a better distribution of the agglomerating binder in the mixture and a quicker fluidification of the mixture.
- Advantageously, the water is added to the mixture in a nebulised form. This makes it possible to speed up the interaction between the agglomerating binder and the water, and in particular between the cellulose, methylcellulose or a mixture of such two compounds and the water, so as to favour the distribution of the agglomerating binder in the mixture and the fluidification of said mixture.
- Operatively, the water essentially performs the function of favouring the mixture of the powders, and in particular of the cellulose, methylcellulose or mixture thereof with the other components.
- Advantageously, as a reinforcing fibre, filaments composed substantially of carbon are used. The expression "filaments composed substantially of carbon" is intended to include, in particular, fibrous materials obtained by pyrolysis of various products of synthetic origin, for example, polyacrylonitrile (PAN) and polisilazane, or of natural origin, for example, tars, cellulose-based natural sources such as vegetable fibres and wood.
- The reinforcing fibres may be previously coated with a protective resin, preferably polyurethane, before being used in the method according to the invention.
- Alternatively, the reinforcing fibres may be previously coated with the same organic agglomerating binder used for the preparation of the mixture. This way a greater cohesion of the material and a more compact product is obtained.
- According to a preferred form of implementation of the invention, the aforesaid organic agglomerating binder additive consists only of cellulose, methyl cellulose or a mixture of cellulose and methyl cellulose. In other words, the mixture does not contain an organic binder resin, and in particular does not contain phenolic resin.
- In particular, according to said preferred form of implementation of the method, the aforesaid mixture comprises:
- between 35% and 50% by weight of reinforcing fibres;
- between 15% and 25% by weight of cellulose, methylcellulose or a mixture of cellulose and methylcellulose;
- at least 20% by weight of fillers; and
- up to 10% by weight of water.
- Preferably, the mixture comprises at least 20% by weight of powder fillers, selected from the group consisting of coke, silicon carbide, graphite or a mixture thereof.
- Advantageously, according to said preferred form of implementation of the method, the step b) is conducted at a temperature not exceeding 50°C, preferably at ambient temperature.
- Alternatively, in order to give greater consistency to the semi-finished product, the forming step can be conducted at a temperature between 50 °C and 100 °C.
- Advantageously, again according to said preferred form of implementation of the method, the infiltration step c) with molten silicon is conducted immediately after the forming step b), without intermediate thermal treatments. In particular, the production method does not comprise an intermediate stage of pyrolysis and the semi-finished product obtained at the end of the forming step b) is directly subjected to infiltration with silicon.
- From experimental tests carried out, it has been seen that the semi-finished product obtained at the end of the forming step b) has a good consistency and density of the order of 1.0-1.1 g/cm3. The semi-finished product can be easily handled without any particular risk of fractures and can be transferred directly from the mould into the furnace for infiltration.
- In particular, the production method has been tested with a mixture having the following composition: 40% fibre, 34% of coke in powder of different particle sizes, 20% of methyl cellulose powder, 10% water, 6% of additives. Carbon fibres are used as fibre. The powder components were mixed with each other gradually; to this powder mixture the fibres and the water in nebulised form were added. The mixture thus obtained was uniaxially pressed in a mould at a pressure of about 68 kg/cm2 at a temperature of 25°C for 10 minutes. The semi-finished product obtained at the end of the forming step showed good consistency such as to allow its manipulation without loss of form and size and had a density of the order of 1.0-1.1 g/cm3. The composite carbon-ceramic material obtained at the end of the infiltration step (conducted directly on the semi-finished product obtained from the forming step without intermediate pyrolysis) presented good characteristics of mechanical resistance.
- According to an alternative form of implementation of the invention, the aforesaid organic agglomerating binder additive comprises: cellulose, methylcellulose or a mixture of cellulose and methylcellulose; and an organic binder resin. Preferably, the aforesaid organic binder resin is a phenolic resin.
- In particular, according to said alternative form of implementation of the method, the aforesaid mixture comprises:
- between 35% and 50% by weight of reinforcing fibres;
- between 5% and 15% by weight of cellulose, methylcellulose or a mixture of cellulose and methylcellulose;
- not more than 10% by weight of organic resin binder;
- at least 20% of fillers; and
- up to 10% by weight of water.
- Preferably, the mixture comprises at least 20% by weight of powder fillers, selected from the group consisting of coke, silicon carbide, graphite or a mixture thereof.
- Advantageously, again according to said alternative form of implementation of the method, the forming step b) is conducted at a temperature between 50°C and 100 °C.
- Preferably, again according to said alternative form of implementation of the method, the infiltration step c) with molten silicon is preceded by a step d) of pyrolysis of the semi-finished product obtained at the end of the forming step b).
- Advantageously, the aforesaid pyrolysis step d) is conducted for a period of time not exceeding 120 minutes, and preferably between 30 and 60 minutes.
- The use in the mixture of the organic binder resin, and in particular of the phenolic resin makes it possible to increase the density of the semi-finished product obtained at the end of the forming step b). It passes from a density of 1.0- 1.1g/cm3 to density values of 1.4- 1.5 g/cm3.
- The use in the mixture of the organic binder resin, and in particular the phenolic resin, also makes it possible to limit the infiltration of silicon in the material, with consequent protection of the carbon fibres from the reaction with the silicon.
- The amount of phenolic resin introduced to the mixture is therefore considerably lower than the amount provided for in the conventional methods. In fact, a quantity not exceeding 10% by weight is provided for against the amount not less than 35-40% by weight traditionally provided for.
- As already noted, the use of the organic binder resin (in particular) of the phenolic resin does not affect the process times of the forming step b) which remain substantially unchanged (no greater than 10 minutes). Use of the resin requires the following however:
- Conducting the forming step at a temperature comprised between 50 °C and 100°C; and
- Performing a pyrolysis step d) between the forming step b) and the infiltration step c).
- As already said, the times of the additional step d) of pyrolysis are, however, very low (in the order of 1-2 hours) and in any case lower than the conventional methods, which provide for pyrolysis steps lasting several hours, typically between 8 and 24 hours.
- Advantageously, the mixture may comprise a component selected from the group consisting of: boron nitride; silicon nitride; kaolin; clay; or metals, such as titanium, chromium, iron, aluminium; or a mixture thereof.
- Such one or more components are added in said mixture in powder form. Preferably, such one or more components are present in the mixture in an amount not exceeding 5% by weight. The introduction in the mixture of such components makes it possible to increase the density of the semi-finished product obtained at the end of the forming step b) and to reduce the infiltration of silicon in the semi-finished product, with consequent protection of the carbon fibres from the reaction with the silicon.
- The present invention relates to a composite carbon-ceramic material, characterised in that it is made with the production method according to the invention, and in particular as described above.
- The present invention relates to a component of a disc brake, characterised in that it is made at least in part with a composite carbon-ceramic material made using the production method according to the invention, and in particular as described above. Preferably, the aforesaid component of a disc brake is a brake disc.
- The invention permits several advantages to be achieved, in part already described.
- The production method of a composite, fibre-reinforced carbon-ceramic material according to the present invention permits increased productivity in terms of energy saving and production times, obtaining a final composite carbon-ceramic material having comparable properties to the materials obtained with conventional methods.
- Thanks to the invention, the forming step can be carried out in very short times and at temperatures not exceeding 100 °C. Advantageously, it is also possible to perform the forming step at a temperature below 50°C, even operating at ambient temperature. This way the forming (or moulding) time is significantly shorter, reducing machine times with a consequent increase in production.
- It should be noted in particular that, it being no longer necessary to heat the mould to a temperature of 150°C, the waiting times required for the cooling of the mould before it can be handled are also reduced.
- Thanks to the invention, it is also possible at least to significantly reduce the time of the pyrolysis step, to the further advantage of economy of the production process.
- According to a preferred embodiment of the invention, it is also possible to obtain the composite carbon-ceramic material without subjecting the semi-finished product obtained in the forming step to pyrolysis. In this case, the moulded semi-finished product can pass directly to the infiltration step with silicon. This entails a further reduction in costs and production times.
- The invention thus conceived thereby achieves the intended objectives.
- Obviously, its practical embodiments may assume forms and configurations different from those described while remaining within the sphere of protection of the invention.
- Moreover, all the details can be replaced by technically equivalent elements and the dimensions, forms and materials used may be any as needed.
Claims (19)
- Method for the production of a composite, fibre-reinforced carbon-ceramic material comprising at least the following operating steps:a) preparing a mixture comprising at least reinforcing fibres and an organic agglomerating binder;b) forming the mixture to obtain a semi-finished product;c) infiltrating the semi-finished product with molten silicon, subjecting the semi-finished product to a firing in the presence of silicon at a temperature such as substantially to bring about the fusion of said silicon and its infiltration into said semi-finished product thus obtaining a composite, fibre-reinforced carbon-ceramic material,characterised in that said organic agglomerating binder, essential for the forming of such material, is present between 15% and 25% by weight of said mixture and comprises cellulose, methyl cellulose or a mixture of cellulose and methyl cellulose and is added to said mixture together with water and in that said forming step is conducted at a temperature not exceeding 100 °C.
- Method according to claim 1, wherein said forming step is conducted for a period of time not exceeding 10 minutes, and preferably between 5 and 10 minutes.
- Method according to claim 1 or 2, wherein said forming step is conducted by exerting on the mixture a pressure between 20 and 100 kg/cm2.
- Method according to claim 1, 2 or 3, wherein said organic agglomerating binder is added to the mixture in powder form.
- Method according to one or more of the claims from 1 to 4, wherein the water is added to said mixture in nebulised form.
- Method according to one or more of the preceding claims, wherein said organic agglomerating binder additive consists only of cellulose, methyl cellulose or a mixture of cellulose and methyl cellulose.
- Method according to claim 6, wherein said mixture comprises between 35% and 50% by weight of reinforcing fibres, between 15% and 25% by weight of cellulose, methyl cellulose or a mixture of cellulose and methyl cellulose, at least 20% by weight of fillers and up to 10% by weight of water.
- Method according to claim 6 or 7, wherein said forming step b) is conducted at a temperature not exceeding 50 °C, preferably at ambient temperature.
- Method according to claim 6 or 7, wherein said forming step b) is conducted at a temperature between 50 °C and 100 °C to give said semi-finished product greater consistency.
- Method according to one or more of claims 6 to 9, wherein said step c) of infiltration with molten silicon is conducted immediately after the forming step b), without intermediate thermal treatments.
- Method according to one or more of the claims from 1 to 5, wherein said organic agglomerating binder additive comprises cellulose, methyl cellulose or a mixture of cellulose and methyl cellulose and an organic resin binder, preferably a phenolic resin.
- Method according to claim 11, wherein said mixture comprises between 35% and 50% by weight of reinforcing fibres, between 5% and 15% by weight of cellulose, methyl cellulose or a mixture of cellulose and methyl cellulose, no more than 10% by weight of organic resin binder, at least 20% of fillers and up to 10% by weight of water.
- Method according to claim 12 or 13, wherein said forming step b) is conducted at a temperature between 50 °C and 100 °C.
- Method according to claim 11, 12 or 13, wherein said step c) of infiltration with molten silicon is preceded by a step d) of pyrolysis of the semi-finished product obtained at the end of the forming step c).
- Method according to claim 14, wherein said pyrolysis step d) is conducted for a period of time not exceeding 120 minutes, and preferably between 30 and 60 minutes.
- Method according to one or more of the preceding claims, wherein said mixture comprises at least 20% by weight of powder fillers, selected from the group consisting of coke, silicon carbide, graphite or a mixture thereof.
- Method according to one or more of the preceding claims, wherein said mixture comprises up to 5% by weight of a component selected from the group consisting of boron nitride, silicon nitride, kaolin, clay, or metals, such as titanium, chromium, iron, aluminium, or a mixture thereof, added to said mixture in powder form.
- Composite carbon-ceramic material, characterised in that it is obtained with the production method according to one or more of the preceding claims.
- Component of a disc brake, characterised in that it is made at least in part with a composite carbon-ceramic material obtained with the production method according to one or more of the claims from 1 to 17, preferably said component of a disc brake being a brake disc.
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ITUB2015A002748A ITUB20152748A1 (en) | 2015-07-31 | 2015-07-31 | METHOD FOR THE PRODUCTION OF A COMPOSITE CARBO-CERAMIC MATERIAL REINFORCED WITH FIBER, COMPOSITE CARBO-CERAMIC MATERIAL OBTAINED WITH THIS METHOD AND COMPONENT OF A DISC BRAKE MADE OF SUCH MATERIAL |
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EP3124455B1 EP3124455B1 (en) | 2018-07-25 |
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DE19820832A1 (en) * | 1998-05-09 | 1999-10-21 | Daimler Chrysler Ag | Production of a solid body used, e.g., as brake disk |
US20020142146A1 (en) * | 1997-03-21 | 2002-10-03 | Daimlerchrysler Ag | Melted-infiltrated fiber-reinforced composite ceramic |
US20030003286A1 (en) * | 2000-09-26 | 2003-01-02 | Udo Gruber | Friction body or sliding body formed from composite materials reinforced with fiber bundles and containing a ceramics matrix and process for the production of a friction or sliding body |
JP2006265434A (en) | 2005-03-25 | 2006-10-05 | Toray Ind Inc | Epoxy resin composition and fiber-reinforced composite material |
US20130284558A1 (en) * | 2010-12-28 | 2013-10-31 | Sgl Carbon Se | Friction discs having a structured ceramic friction layer and method of manufacturing the friction discs |
US8883938B2 (en) | 2009-09-18 | 2014-11-11 | Dic Corporation | Resin composition for fiber-reinforced composite material, cured product thereof, fiber-reinforced composite material, molding of fiber-reinforced resin, and process for production thereof |
WO2016055975A1 (en) * | 2014-10-10 | 2016-04-14 | Petroceramics S.P.A. | Method for making brake discs in material reinforced with fibres and brake disc made with such method |
-
2015
- 2015-07-31 IT ITUB2015A002748A patent/ITUB20152748A1/en unknown
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2016
- 2016-07-29 EP EP16182028.7A patent/EP3124455B1/en active Active
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US20020142146A1 (en) * | 1997-03-21 | 2002-10-03 | Daimlerchrysler Ag | Melted-infiltrated fiber-reinforced composite ceramic |
DE19820832A1 (en) * | 1998-05-09 | 1999-10-21 | Daimler Chrysler Ag | Production of a solid body used, e.g., as brake disk |
US20030003286A1 (en) * | 2000-09-26 | 2003-01-02 | Udo Gruber | Friction body or sliding body formed from composite materials reinforced with fiber bundles and containing a ceramics matrix and process for the production of a friction or sliding body |
JP2006265434A (en) | 2005-03-25 | 2006-10-05 | Toray Ind Inc | Epoxy resin composition and fiber-reinforced composite material |
US8883938B2 (en) | 2009-09-18 | 2014-11-11 | Dic Corporation | Resin composition for fiber-reinforced composite material, cured product thereof, fiber-reinforced composite material, molding of fiber-reinforced resin, and process for production thereof |
US20130284558A1 (en) * | 2010-12-28 | 2013-10-31 | Sgl Carbon Se | Friction discs having a structured ceramic friction layer and method of manufacturing the friction discs |
WO2016055975A1 (en) * | 2014-10-10 | 2016-04-14 | Petroceramics S.P.A. | Method for making brake discs in material reinforced with fibres and brake disc made with such method |
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ITUB20152748A1 (en) | 2017-01-31 |
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